JPS6260474B2 - - Google Patents
Info
- Publication number
- JPS6260474B2 JPS6260474B2 JP59117784A JP11778484A JPS6260474B2 JP S6260474 B2 JPS6260474 B2 JP S6260474B2 JP 59117784 A JP59117784 A JP 59117784A JP 11778484 A JP11778484 A JP 11778484A JP S6260474 B2 JPS6260474 B2 JP S6260474B2
- Authority
- JP
- Japan
- Prior art keywords
- pair
- hydrogen
- electrode plates
- gas
- oxyhydrogen
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
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Classifications
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
- C25B1/00—Electrolytic production of inorganic compounds or non-metals
- C25B1/01—Products
- C25B1/02—Hydrogen or oxygen
- C25B1/04—Hydrogen or oxygen by electrolysis of water
- C25B1/044—Hydrogen or oxygen by electrolysis of water producing mixed hydrogen and oxygen gas, e.g. Brown's gas [HHO]
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
- C25B9/00—Cells or assemblies of cells; Constructional parts of cells; Assemblies of constructional parts, e.g. electrode-diaphragm assemblies; Process-related cell features
- C25B9/07—Common duct cells
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
- C25B9/00—Cells or assemblies of cells; Constructional parts of cells; Assemblies of constructional parts, e.g. electrode-diaphragm assemblies; Process-related cell features
- C25B9/17—Cells comprising dimensionally-stable non-movable electrodes; Assemblies of constructional parts thereof
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
- C25B9/00—Cells or assemblies of cells; Constructional parts of cells; Assemblies of constructional parts, e.g. electrode-diaphragm assemblies; Process-related cell features
- C25B9/17—Cells comprising dimensionally-stable non-movable electrodes; Assemblies of constructional parts thereof
- C25B9/19—Cells comprising dimensionally-stable non-movable electrodes; Assemblies of constructional parts thereof with diaphragms
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/36—Hydrogen production from non-carbon containing sources, e.g. by water electrolysis
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S204/00—Chemistry: electrical and wave energy
- Y10S204/05—Magnetic plus electrolytic
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
Description
【発明の詳細な説明】
(a) 産業上の利用分野
この発明は、同一機から同時かつ継続的に酸素
ガスと水素ガスとを互に混合乃至分離可能な状態
で生成させる装置に関する。DETAILED DESCRIPTION OF THE INVENTION (a) Field of Industrial Application This invention relates to an apparatus for simultaneously and continuously producing oxygen gas and hydrogen gas in a state in which they can be mixed or separated from each other from the same machine.
酸素または水素を互に別個独自に生成する装置
が従来多数存在すること周知であり、本発明もま
た上記の分離生成を容易に可能とするが、この発
明の主たる目的は、むしろ、同一機から同時に酸
水素混合ガスを発生せしめ得る点に多くの利益を
見出さんとするものである。 It is well known that there are a number of devices that produce oxygen or hydrogen separately and independently from each other, and the present invention also facilitates the above-mentioned separate production, but the main purpose of this invention is rather to The idea is to find many benefits in being able to generate an oxyhydrogen mixed gas at the same time.
何故ならば、水素と酸素とは互いに反応して常
温では水を生成するが、その反応を電気火花また
は白金触媒によつて促進させると、爆発的な激し
さで発熱反応し、例えば25℃、1気圧で
68.313Kcal/molの熱を出し、そのときの温度が
2800℃にも達することがあるので、酸水素トーチ
として、鋼板の溶接や切断またはガラスの変形な
どの熱処理加工に有益であるばかりか、直接的な
熱源乃至光源として利用することもまた容易に可
能である。 This is because hydrogen and oxygen react with each other to produce water at room temperature, but when this reaction is accelerated by an electric spark or a platinum catalyst, an exothermic reaction occurs with explosive intensity, for example at 25°C. at 1 atm
It produces heat of 68.313Kcal/mol, and the temperature at that time is
Since it can reach up to 2800℃, it is not only useful as an oxyhydrogen torch for heat treatment processes such as welding and cutting steel plates or deforming glass, but it can also be easily used as a direct heat source or light source. It is.
酸素と水素の混合ガスを利用した溶接(以下酸
水素溶接という)は、他の溶接法、例えば、アセ
チレン酸素ガス溶接、アーク溶接または電気抵抗
溶接などと比較して、次の点、すなわち、溶接加
工時に生ずる酸化及び窒化の現象を少くするの
で、酸化し易い金属、軽合金およびニツケルクロ
ーム鋼などの溶接に際して肉盛、切断等から生ず
る機械的性質の変相乃至変態が小さい点、及び、
当初の強度乃至硬度を何ら低下させずその侭維持
し得る点などが有利であるとされている。 Welding using a mixed gas of oxygen and hydrogen (hereinafter referred to as oxyhydrogen welding) has the following points compared to other welding methods, such as acetylene oxygen gas welding, arc welding, or electric resistance welding. Since it reduces oxidation and nitridation phenomena that occur during processing, phase changes or transformations in mechanical properties that occur from overlaying, cutting, etc. when welding easily oxidized metals, light alloys, nickel chrome steel, etc. are small; and
It is said to be advantageous in that the original strength or hardness can be maintained without any reduction.
(b) 従来の技術
しかしながら、例えば従来における酸水素溶接
では、いわゆるボンベと称する厚肉の継目なし鋼
製シリンダ型容器の中に別個に圧縮充填された高
圧の酸素ガス及び水素ガスを、所定の、例えば
1:4の比率で混合して使用していたので、ボン
ベが重くて作業の機動性乃至可搬性が劣悪である
ばかりか、高圧ガス取扱上生ずる多くの危険に備
えて厳重な取締規則が存在すること周知の通りで
ある。(b) Prior art However, in conventional oxyhydrogen welding, for example, high-pressure oxygen gas and hydrogen gas, which are separately compressed and filled into a thick-walled seamless steel cylinder-type container called a cylinder, are For example, since the cylinders were mixed at a ratio of 1:4, the cylinders were heavy and had poor maneuverability and portability, as well as strict regulations to prevent the many dangers that arise when handling high-pressure gas. It is well known that there exists
そこで、常圧下で手軽に酸水素混合ガスを継続
供給し得る装置が開発されれば、酸水素溶接時等
における前記の憂いが一挙に解消されるであろ
う。 Therefore, if a device capable of easily and continuously supplying an oxyhydrogen mixed gas under normal pressure is developed, the above-mentioned concerns during oxyhydrogen welding, etc. will be eliminated at once.
従来周知の酸水素混合ガス生成手段は、次の電
気分解によるものがあり、その基本的な構成と作
用は、電気抵抗値が最小の電解液、例えば、20%
の水酸化ナトリウム(NaOH)、または、30%の
カセイカリ(KOH)の大溶液中に一対の電極を
併設し、その電極間に直流電流を通ぜしめると、
イオン導電体となつた水溶液中の陽イオンを陰極
へ、陰イオンが陽極へ向つて移動し、それに伴な
つて、電極とイオン導電体との界面で化学反応が
起り、陽極から酸素(O2)が、陰極から水素
(H2)が、1:2の割合で気泡となつて発生す
る。 Conventionally known oxyhydrogen mixed gas generation means include the following electrolysis method, whose basic structure and operation are as follows: An electrolytic solution with the minimum electrical resistance value, for example, 20%
When a pair of electrodes is placed in a large solution of 30% sodium hydroxide (NaOH) or 30% caustic potash (KOH) and a direct current is passed between the electrodes,
The cations in the aqueous solution that have become ionic conductors move toward the cathode, and the anions move toward the anode. Along with this, a chemical reaction occurs at the interface between the electrode and the ionic conductor, and oxygen (O 2 ) is removed from the anode. ), hydrogen (H 2 ) is generated as bubbles from the cathode at a ratio of 1:2.
発生する気泡の量と電気量との間にはフアラデ
ーの法則が成り立ち、両者は互に比例するので、
気泡群の発生を多量に期待する場合には、それに
相当する大容量の電場エネルギーが必要とされ
る。 Faraday's law holds between the amount of bubbles generated and the amount of electricity, and the two are proportional to each other, so
If a large number of bubble groups are expected to be generated, a correspondingly large amount of electric field energy is required.
しかしながら、電極板面に発生する気泡は一様
に小粒であつて、気泡自体が有する浮力では板面
から離れて浮上する力が足りず、小気泡群が或る
値以上のトータル浮力に達したとき、電極板面か
ら離脱して浮上し、とりわけ、多数の電極板を過
密に併設した場合に気泡の浮上が一様でない傾向
にあり、このようなガスの断続的な浮上現象はガ
スの継続的定量供給を必要とする場合に甚だ不都
合である一方、電極板面に付着する気泡群が絶縁
層となつて作用し、導電能力を低下させ電解生成
を鈍化させる憂いがあつた。 However, the bubbles generated on the electrode plate surface are uniformly small particles, and the buoyancy of the bubbles themselves is not enough to float away from the plate surface, and the group of small bubbles reaches a total buoyancy of more than a certain value. In particular, when a large number of electrode plates are placed closely together, the levitation of gas bubbles tends to be uneven. This is extremely inconvenient when a fixed quantity supply is required, and there is also the concern that the bubbles adhering to the surface of the electrode plate act as an insulating layer, lowering the electrical conductivity and slowing down electrolytic production.
上記の不都合を解消する一手段として、電場エ
ネルギーを常時過大に設定して、気泡群の発生能
力それ自体を高めることが考えられるが、大電力
が長時間にわたつて継続して消費される憂いがあ
つた。 One way to solve the above-mentioned problems is to constantly set the electric field energy too high to increase the ability to generate bubbles, but this would cause the problem of continuously consuming a large amount of power over a long period of time. It was hot.
(c) 発明が解決しようとする問題点
この発明の第1の目的は、上記の不都合を一掃
して、浮力の足りない小粒の気泡であつても電極
板面から速やかに離脱浮上させて、酸水素ガスの
継続的定量供給を可能ならしめると共に、導電能
力を良好に保持して電場エネルギーを常時有効に
活用し得る酸水素ガス同時生成機を創作して提供
することである。(c) Problems to be Solved by the Invention The first object of the invention is to eliminate the above-mentioned disadvantages, and to quickly separate and float even small bubbles with insufficient buoyancy from the electrode plate surface. An object of the present invention is to create and provide an oxyhydrogen gas simultaneous generator that enables continuous quantitative supply of oxyhydrogen gas, maintains good conductivity, and effectively utilizes electric field energy at all times.
この発明の第2の目的は、電場エネルギーとし
て消費される電力の供給を必要最少限に抑制する
ことができ、かつ、消費される水の量が生成ガス
の1/1800の少量で足りる経済的な酸水素ガス同時
生成機を創作して提供することである。 The second object of this invention is to reduce the supply of electric power consumed as electric field energy to the necessary minimum, and to achieve an economical system in which the amount of water consumed is as small as 1/1800 of the generated gas. The purpose of this invention is to create and provide an oxyhydrogen gas simultaneous generator.
この発明の第3の目的は、酸素と水素の混合ガ
ス生成に際し、従来慣用の高圧ボンベ詰めのもの
を使用せず、取扱操作と移動とが容易かつ安全な
酸水素ガス同時生成機を創作して提供することで
ある。 The third object of this invention is to create an oxyhydrogen gas simultaneous generation machine that is easy to handle and move, and is safe, without using conventional high-pressure cylinders when generating a mixed gas of oxygen and hydrogen. The goal is to provide the following information.
この発明の第4の目的は、酸素ガスと水素ガス
とを混合状態で、または相互分離状態で容易に取
り出し得る酸水素ガス同時生成機を創作して提供
することである。 A fourth object of the present invention is to create and provide an oxyhydrogen gas simultaneous generator that can easily extract oxygen gas and hydrogen gas in a mixed state or in a mutually separated state.
この発明の第5の目的は、従来型で生成される
水素の性質が引火性の強い危険なオルト水素であ
つたのに対し、引火性の弱い安全かつ安定したパ
ラ水素を生成し得る装置を得ることである。 The fifth object of this invention is to provide an apparatus that can generate safe and stable para-hydrogen, which is less flammable, whereas the hydrogen produced by conventional methods is highly flammable and dangerous ortho-hydrogen. It's about getting.
この発明の第6の目的は、燃焼すれば水に戻つ
て公害の生じない酸水素同時生成機を得ることで
ある。 The sixth object of the present invention is to obtain an oxyhydrogen co-generator that does not cause pollution because it returns to water when burned.
この発明の第7の目的は、用途として、常圧及
び負圧または水中を含む環境下における溶接溶断
加工が可能であり、一般的及び車両用の燃料とし
て使うことができ、更に、ガラス細工、光フアイ
バ加工、半導体加工に利用することができ、空気
の清浄化にも役立ち得る酸水素同時生成機を得る
ことである。 A seventh object of the present invention is that it can be used for welding and cutting under normal pressure, negative pressure, or underwater environments, can be used as fuel for general and vehicles, and can be used for glass work, The object of the present invention is to obtain an oxyhydrogen simultaneous generator that can be used for optical fiber processing and semiconductor processing, and can also be useful for air purification.
(d) 問題点を解決するための手段
この発明は、上記の目的を達成するために、上
面に気体取出孔のある水槽内に、少なくとも一対
の正負電極板を対設する一方、その一対の電極板
間に生ずる電位差の方向と関連させてフレミング
左手3指の法則により力が上方へ向くように、少
なくとも一対の磁性体をその極性を同一方向に向
けて配設することによつて、酸水素混合ガスを同
時に生成するものである。(d) Means for Solving the Problems In order to achieve the above-mentioned object, the present invention provides at least one pair of positive and negative electrode plates facing each other in a water tank having a gas outlet hole on the upper surface. By arranging at least a pair of magnetic materials with their polarities facing in the same direction so that the force is directed upward according to Fleming's three-fingered rule in relation to the direction of the potential difference generated between the electrode plates, the acid It simultaneously generates hydrogen mixed gas.
酸素と水素とを分離して取り出すには一対の電
極板間に隔膜を介挿すると共に取出孔を別設する
ことによつて達成される。 Separating and extracting oxygen and hydrogen can be achieved by interposing a diaphragm between a pair of electrode plates and providing a separate extraction hole.
先ず、第1図において、槽4内には注水孔6を
経由して電気抵抗値の小さな電解水溶液8が充た
されており、その水溶液中には陽極10と陰極1
2とから成る一対の電極板が併設されている。 First, in FIG. 1, a tank 4 is filled with an electrolytic aqueous solution 8 having a small electric resistance value through a water injection hole 6, and an anode 10 and a cathode 1 are placed in the aqueous solution.
A pair of electrode plates consisting of 2 are also provided.
そこで、その電極間に槽外の直流電源14から
直流電流を通ぜしめると、両極間に電位差が生じ
て矢印16の方向の電場が形成され、水溶液8が
イオン導電体となり、溶液中の陽イオンが陰極1
2へ、陰イオンが陽極10へ向つて移動し、陽極
10の界面から酸素の気泡が、陰極12の界面か
ら水素の気泡が1:2の割合で発生する。 Therefore, when a DC current is passed between the electrodes from the DC power supply 14 outside the tank, a potential difference is generated between the two electrodes, and an electric field in the direction of the arrow 16 is formed, and the aqueous solution 8 becomes an ionic conductor, and the positive ions in the solution Ion is cathode 1
2, anions move toward the anode 10, and oxygen bubbles are generated from the anode 10 interface and hydrogen bubbles are generated from the cathode 12 interface at a ratio of 1:2.
上記の構成と作用は従来周知の水電解による酸
水素生成手段に外ならず、本発明は上記手段が有
する欠陥を改善したものである。 The above-mentioned structure and operation are equivalent to the conventional means for generating oxyhydrogen by water electrolysis, and the present invention improves the deficiencies of the above-mentioned means.
すなわち、両極とイオン導電体との界面に生成
された酸素と水素の気泡群は、当初、各自が保有
する浮力のみでは極面から自力で離脱し得ない
程、微細な小気泡群に過ぎないため、各極面にそ
れらの小気泡群が密集して付着し、付着した小気
泡群が電場16を遮断する絶縁層となつて作用
し、界面における気泡生成能力が劣化するので、
それでは酸水素ガスの定量継続供給が保証されな
い。 In other words, the oxygen and hydrogen bubbles generated at the interface between the poles and the ionic conductor are initially so small that they cannot separate from the pole surface on their own using only their own buoyancy. Therefore, these small bubbles adhere densely to each pole surface, and the attached small bubbles act as an insulating layer that blocks the electric field 16, deteriorating the bubble generation ability at the interface.
This does not guarantee constant constant supply of oxyhydrogen gas.
そこで、本発明では、電場16に対して、フレ
ミング左手3指の法則に従つた方向、すなわち、
第1図において、手前から先方へ向う電場16に
直交して左から右へ向う磁場18を設定するため
に、一対の強力な磁性体20及び22を併設すれ
ば、フレミング左手3指の法則に従つて上方への
力Fが発生する。 Therefore, in the present invention, the electric field 16 is directed in a direction according to Fleming's left hand three finger rule, that is,
In FIG. 1, if a pair of strong magnetic bodies 20 and 22 are installed in order to set the magnetic field 18 that goes from left to right orthogonal to the electric field 16 that goes from the front to the front, Fleming's three-finger rule on the left hand is satisfied. Therefore, an upward force F is generated.
(e)作用
いままで浮力不足によつて電極面に付着を余儀
なくされていた小気泡群が、前記の力Fを受け
て、電場16にも磁場18にも垂直な方向、すな
わち上方へ高速でドリフトするのが認められる。(e) Effect The small bubbles, which had until now been forced to adhere to the electrode surface due to lack of buoyancy, are subjected to the above force F and are moved at high speed in a direction perpendicular to both the electric field 16 and the magnetic field 18, that is, upward. Drifting is allowed.
換言すれば、各気泡はそれ自体の浮力に前記ド
リフトの力が加えられることによつて、電極面か
らの付着力を絶ち切ることができ、水面に向つて
浮上運動することが可能となる。 In other words, each bubble can break off the adhesion force from the electrode surface by adding the drift force to its own buoyant force, and can float toward the water surface.
このドリフトによる浮上運動は、酸素ガス及び
水素ガスの双方に共通して一様に認められるよう
であるが、とりわけ水素ガスについては次の推定
が成り立つものと思われる。 It seems that this floating movement due to drift is uniformly observed in both oxygen gas and hydrogen gas, but the following assumption seems to hold especially true for hydrogen gas.
周知のように、水素は分子1個について2個の
原子核が自転(スピン)しており、そのスピンの
方向が互に同一方向のものをオルト水素と称し、
互に逆方向のものをパラ水素と称し、常温乃至そ
れ以上の状態ではオルト3に対しパラ1の割合で
存在するが、水素分子がオルトの状態下では原子
核間に斥力がはたらいて不安定であり、パラの状
態下では原子核間に引力がはたらいて安定すなわ
ち活性化の状態にあるとされており、磁性体を触
媒に使うことによつて不安定なオルト水素を安定
なパラ水素に転換することが可能であるとされて
いる。 As is well known, hydrogen has two atomic nuclei that rotate (spin) per molecule, and those whose spin directions are in the same direction are called ortho-hydrogen.
Hydrogen in opposite directions is called para-hydrogen, and at room temperature or above, it exists in a ratio of 3 ortho to 1 para, but when the hydrogen molecules are ortho, there is a repulsion between the nuclei and it becomes unstable. It is said that under the para state, an attractive force acts between the atomic nuclei, resulting in a stable or activated state, and by using a magnetic material as a catalyst, unstable ortho-hydrogen is converted to stable para-hydrogen. It is said that this is possible.
従つて、本発明において、電場16と磁場18
とが直交するなかに水素分子を置いた場合に、力
Fの方向がオルト水素の回転方向と逆であると仮
定すれば、そのオルト水素はパラ水素に転換され
るであろうし、前記力Fの方向がパラ水素の回転
方向と一致すると仮定すれば、パラ水素は更に加
速して浮上するであろうことが推定される。 Therefore, in the present invention, the electric field 16 and the magnetic field 18
If a hydrogen molecule is placed perpendicular to F, and assuming that the direction of force F is opposite to the direction of rotation of ortho-hydrogen, the ortho-hydrogen will be converted to para-hydrogen, and the force F If it is assumed that the direction of is the same as the rotation direction of para-hydrogen, it is estimated that para-hydrogen will further accelerate and rise to the surface.
このようにして、気泡の浮上運動が迅速かつ間
断なく実現されると、電極面に残存付着する気泡
群が常時一掃されるので、各電極面はイオン導電
体としての水溶液を再び電極反応の進行に役立た
しめ得るから、電解効果が著しく促進され、電場
エネルギーが小さくても効率のよい気泡生成が達
成される。 In this way, when the floating movement of the bubbles is achieved quickly and without interruption, the bubbles remaining on the electrode surface are constantly wiped out, and each electrode surface reuses the aqueous solution as an ionic conductor for the progress of the electrode reaction. Therefore, the electrolytic effect is significantly promoted, and efficient bubble generation can be achieved even with small electric field energy.
(f) 実施例
この発明の具体的一実施例を第2図及び第3図
によつて以下に詳述する。(f) Embodiment A specific embodiment of the present invention will be described in detail below with reference to FIGS. 2 and 3.
角形の槽4には蓋5があり、その蓋にはねじ栓
7のついた注水孔6と、気体取出孔9とが設けら
れ、槽4は電解水溶液8で充たされている。 The rectangular tank 4 has a lid 5, and the lid is provided with a water injection hole 6 with a screw stopper 7 and a gas outlet hole 9, and the tank 4 is filled with an electrolytic aqueous solution 8.
槽内底の左右端にそれぞれサイドフレーム23
及び24が併設され、各フレームの上部間及び下
部間にはそれぞれ端子棒25及び26が架設さ
れ、上部端子棒25には等間隔のスペーサ27,
27a,27b…を介して非磁性材の上部電極板
(例えば陽極10)を列設する一方、下部端子棒
26にも等間隔のスペーサ28,28a,28b
…を介して非磁性材の下部電極板(例えば陰極1
2)を列設し、両電極板を交互に等間隔かつ非接
触の状態で噛み合わせると、正負電極板の対が何
れも同一方向の電位差が生じるように配列される
ので、各電極板に共通の電場(第1図16参照)
が形成される。 Side frames 23 are installed at the left and right ends of the bottom of the tank.
Terminal bars 25 and 26 are installed between the upper and lower parts of each frame, respectively, and the upper terminal bar 25 has spacers 27 and 24 arranged at equal intervals.
Upper electrode plates (for example, anodes 10) made of non-magnetic material are arranged in a row via 27a, 27b, etc., and spacers 28, 28a, 28b are also arranged at equal intervals on the lower terminal bar 26.
... through the lower electrode plate of non-magnetic material (for example, the cathode 1
2) are arranged in a row and the two electrode plates are interlocked alternately at equal intervals and in a non-contact state, the pairs of positive and negative electrode plates are arranged so that a potential difference occurs in the same direction. Common electric field (see Figure 1, 16)
is formed.
他方において、この積層電極板の手前側と向う
側にそれぞれ極性が同一方向の環状の永久磁石2
2及び20を配設すると、前記電場に直交する状
態で磁場(第1図18参照)が形成される。29
及び30は磁石をサイドフレームに固定するため
の取付ボルトである。 On the other hand, annular permanent magnets 2 with polarity in the same direction are placed on the front side and the opposite side of this laminated electrode plate, respectively.
2 and 20, a magnetic field (see FIG. 18) is created perpendicular to the electric field. 29
and 30 are mounting bolts for fixing the magnet to the side frame.
本発明装置を酸水素溶接乃至切断に使用する場
合には、例えば第1図で示すように、気体取出孔
9にフレキシフルなガス導管31を取り付け、そ
の導管の先端に火口ノズル32を取り付け、着火
させると、ノズルから吹き出す酸水素混合ガス火
焔33となるので、直ちに使用することができ
る。 When the device of the present invention is used for oxyhydrogen welding or cutting, for example, as shown in FIG. When ignited, an oxyhydrogen mixed gas flame 33 is blown out from the nozzle, so it can be used immediately.
同時に生成された酸素ガスと酸素ガスとを分離
して取り出すには、周知のように、陰陽電極板間
に隔膜(図示せず)を介設すると共に蓋面に酸素
と水素とを別個に取り出す孔(図示せず)をそれ
ぞれ設けることによつて容易に可能となる。 In order to separate and take out the oxygen gas generated at the same time, as is well known, a diaphragm (not shown) is interposed between the negative and positive electrode plates, and oxygen and hydrogen are taken out separately from the lid surface. This is easily possible by providing holes (not shown) in each case.
分離して取り出された双方のガスは、それぞれ
単独で使用されるのに適しているが、再び混合さ
せて使用することもまた容易である。 Both gases separated and taken out are suitable to be used individually, but it is also easy to mix them together and use them again.
混合取出と分離取出との間の交互切換手段を付
設して、必要に応じて選別して使用し得るように
構成することもまた容易である。 It is also easy to provide a means for alternately switching between mixed take-out and separate take-out so that they can be selectively used as required.
安全対策としては、例えば、万一に備えて万全
を期するため、装置の各所に流量計と安全弁及び
逆火防止手段(図示せず)を設け、電源停止時に
自動排出装置が作動して屋外へ排出される手段を
備える。 As a safety measure, for example, in order to be fully prepared for any emergency, we have installed flowmeters, safety valves, and flashback prevention means (not shown) in various parts of the equipment, and when the power is turned off, an automatic discharge device is activated to prevent outdoor use. It is provided with a means for being discharged to.
(g) 発明の効果
この発明の第1の効果は、電場16に直交させ
て磁場18を設定したことによつて、電極板面に
付着した小気泡群に上方への力Fが与えられるよ
うになつたので、その力Fが気泡群を電極板面1
0及び12から離脱浮上させるのに役立ち、酸水
素ガスの継続的安定供給が保証されるばかりでな
く、いままで電極板面上への小気泡群の残留付着
が絶縁作用をして導電性能を低下させていた弊害
が本発明によつて一掃され、板面における導電能
力を常時最良の状態に保持して電場エネルギーを
有効に活用し得るようになつた。(g) Effect of the Invention The first effect of the invention is that by setting the magnetic field 18 perpendicular to the electric field 16, an upward force F is applied to the group of small bubbles attached to the electrode plate surface. , the force F moves the bubble group toward the electrode plate surface 1.
Not only does it help to float away from 0 and 12, ensuring a continuous and stable supply of oxyhydrogen gas, but also the residual adhesion of small bubbles on the electrode plate surface acts as an insulator and improves conductive performance. The present invention eliminates the adverse effects that had been causing the decline, and it has become possible to maintain the electrical conductivity on the plate surface in the best condition at all times and to effectively utilize the electric field energy.
この発明の第2の効果は、上記第1の効果と関
連して、従来のように電場エネルギーを常時過大
に供給せず、電場形成に必要な最少限の電力供給
で足りるようになつたので、ランニングコストが
低廉である。 The second effect of this invention is related to the first effect, because it is possible to avoid constantly supplying excessive electric field energy as in the conventional case, and it is now sufficient to supply the minimum amount of power necessary to form an electric field. , running costs are low.
この発明の第3の効果は、酸素と水素の混合ガ
ス生成に際して、本発明では常圧でかつ双方同時
に生成し供給し得るから、従来の高圧ボンベ詰め
のものの使用に比して、取扱及び操作において、
とりわけ搬出入移動において、著しく容易かつ安
全である。 The third effect of this invention is that when generating a mixed gas of oxygen and hydrogen, the present invention can simultaneously generate and supply both at normal pressure, making it easier to handle and operate compared to the conventional use of high-pressure cylinders. In,
In particular, it is extremely easy and safe to carry in and out.
この発明の第4の効果は、酸素ガスと水素ガス
とを混合状態でも相互分離状態でも、所望によ
り、きわめて容易に取り出すことが可能である。 A fourth effect of the present invention is that oxygen gas and hydrogen gas can be extracted very easily as desired, whether in a mixed state or in a mutually separated state.
この発明の第5の効果は、発生タンク1個10
を積載するにも拘らず超小型(横34cm、高さ73.5
cm、奥行40cm)であり、それでいて性能は、例え
ば単相AC100ボルト5アンペアの電源を使つて
300乃至400Wの電力を消費し、純度99.9999%の
酸素を毎分、1500乃至2400c.c.発生させることがで
き、そのガス圧力は1cm2当り0.5乃至3.0Kg、発生
するカロリーは25℃1気圧毎分1の消費量で
53.8kcalである。 The fifth effect of this invention is that one generation tank
Ultra-compact (width 34 cm, height 73.5
cm, depth 40cm), and the performance is, for example, using a single-phase AC 100 volt 5 ampere power supply.
It consumes 300 to 400W of power and can generate 1500 to 2400c.c. of 99.9999% pure oxygen per minute, the gas pressure is 0.5 to 3.0Kg per cm2, and the generated calories are 1 atm at 25℃. With a consumption of 1 per minute
It is 53.8kcal.
この発明の第6の効果は、引火性の強い危険な
オルト水素を引火性の弱い安全かつ安定したパラ
水素に転換して生成し得るから安全性が高いこと
である。 The sixth effect of the present invention is that it is highly safe because highly flammable and dangerous ortho-hydrogen can be converted into less flammable, safe and stable para-hydrogen.
この発明の第7の効果は、燃焼の結果、水に戻
るので、何ら公害が発生しない利点がある。 The seventh effect of the present invention is that as a result of combustion, it returns to water, so there is an advantage that no pollution occurs.
この発明の第8の効果は、常圧、負圧、水中に
おける溶断溶接加工、ガラス細工、光フアイバ、
半導体の加工、一般及び車両用燃料、空気の清浄
化等極めて広い範囲で使用可能なことである。 The eighth effect of this invention is that it can be used for fusing welding at normal pressure, negative pressure, and underwater, glass work, optical fiber,
It can be used in an extremely wide range of applications, including semiconductor processing, general and vehicle fuel, and air purification.
第1図は本発明の原理を図示した説明図、第2
図は本発明の具体的一実施態様を例示した縦断正
面図、第3図は槽の前面を破断した斜視図であ
る。
4……槽、5……蓋、6……注水孔、7……ね
じ栓、8……電解水溶液、9……気体取出孔、1
0……陽極例えば上部電極板、12……陰極例え
ば下部電極板、14……直流電源、16……矢印
方向の電位差をもつ電場、18……磁場、20及
び22……磁性体例えば環状の永久磁石、23及
び24……サイドフレーム、25及び26……端
子棒、27,27a,27b……スペーサ、2
8,28a,28b……スペーサ、29及び30
……取付ボルト、F……力の方向、31……ガス
導管、32……火口ノズル、33……火焔。
Figure 1 is an explanatory diagram illustrating the principle of the present invention;
The figure is a longitudinal sectional front view illustrating a specific embodiment of the present invention, and FIG. 3 is a perspective view with the front side of the tank cut away. 4... Tank, 5... Lid, 6... Water injection hole, 7... Screw plug, 8... Electrolytic aqueous solution, 9... Gas extraction hole, 1
0... Anode, e.g., upper electrode plate, 12... Cathode, e.g., lower electrode plate, 14... DC power source, 16... Electric field with a potential difference in the direction of the arrow, 18... Magnetic field, 20 and 22... Magnetic material, e.g., ring-shaped Permanent magnet, 23 and 24... Side frame, 25 and 26... Terminal bar, 27, 27a, 27b... Spacer, 2
8, 28a, 28b...Spacer, 29 and 30
...Mounting bolt, F...Direction of force, 31...Gas conduit, 32...Cinder nozzle, 33...Flame.
Claims (1)
内に対設した少なくとも一対の正負電極板と、そ
の一対の電極板間に生ずる電位差の方向と関連さ
せてフレミング左手3指の法則により力が上方へ
向くようにその極性を同一方向に向けて配設した
少なくとも一対の磁性体と、から成る酸水素混合
ガス同時生成機。 2 上面に酸素と水素とを別個に取り出す孔のあ
る水槽と、その水槽内に対設した少なくとも一対
の正負電極板と、その電極板間に介挿した隔膜
と、その一対の電極板間に生ずる電位差の方向と
関連させてフレミング左手3指の法則により力が
上方へ向くようにその極性を同一方向に向けて配
設した少なくとも一対の磁性体と、から成る酸水
素分離ガス同時生成機。[Claims] 1. Fleming's left hand 3 in relation to a water tank having a gas extraction hole on the top surface, at least one pair of positive and negative electrode plates disposed oppositely in the water tank, and the direction of the potential difference generated between the pair of electrode plates. An oxyhydrogen mixed gas simultaneous generator comprising at least a pair of magnetic materials arranged with their polarities facing in the same direction so that the force is directed upward according to the finger rule. 2. A water tank with holes on the top surface for extracting oxygen and hydrogen separately, at least one pair of positive and negative electrode plates placed opposite each other in the water tank, a diaphragm inserted between the electrode plates, and a diaphragm inserted between the pair of electrode plates. An oxyhydrogen separation gas simultaneous generator comprising: at least a pair of magnetic bodies arranged with their polarities facing in the same direction so that the force is directed upward according to Fleming's left hand three finger rule in relation to the direction of the generated potential difference.
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP59117784A JPS60262986A (en) | 1984-06-08 | 1984-06-08 | Simultaneous forming apparatus of gaseous oxygen and hydrogen |
| US06/878,062 US4747925A (en) | 1984-06-08 | 1986-06-24 | Apparatus for simultaneous generation of oxygen and hydrogen gases |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP59117784A JPS60262986A (en) | 1984-06-08 | 1984-06-08 | Simultaneous forming apparatus of gaseous oxygen and hydrogen |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS60262986A JPS60262986A (en) | 1985-12-26 |
| JPS6260474B2 true JPS6260474B2 (en) | 1987-12-16 |
Family
ID=14720227
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP59117784A Granted JPS60262986A (en) | 1984-06-08 | 1984-06-08 | Simultaneous forming apparatus of gaseous oxygen and hydrogen |
Country Status (2)
| Country | Link |
|---|---|
| US (1) | US4747925A (en) |
| JP (1) | JPS60262986A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0340162U (en) * | 1989-08-22 | 1991-04-17 |
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-
1984
- 1984-06-08 JP JP59117784A patent/JPS60262986A/en active Granted
-
1986
- 1986-06-24 US US06/878,062 patent/US4747925A/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0340162U (en) * | 1989-08-22 | 1991-04-17 |
Also Published As
| Publication number | Publication date |
|---|---|
| US4747925A (en) | 1988-05-31 |
| JPS60262986A (en) | 1985-12-26 |
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